Chemical Properties of 1-Propene, 2-methyl- (CAS 115-11-7)

InChI

InChI=1S/C4H8/c1-4(2)3/h1H2,2-3H3

InChI Key

VQTUBCCKSQIDNK-UHFFFAOYSA-N

Formula

C4H8

SMILES

C=C(C)C

Molecular Weight¹

56.11

CAS

115-11-7

Other Names

• 1,1-Dimethylethene
• 1,1-Dimethylethylene
• 2-Methylpropylene
• 2-methyl-1-propene
• 2-methylprop-1-ene
• 2-methylpropene
• Isopropylidenemethylene
• Methylpropene
• UN 1055
• iso-C4H8
• isobutene
• isobutylene
• propene, 2-methyl-
• «gamma»-Butylene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.1884		Relay (1.0) Calculated Property
PAff	[802.10; 805.00]	kJ/mol
PAff	802.10	kJ/mol	NIST
PAff	802.30 ± 4.80	kJ/mol	NIST
PAff	802.30 ± 4.80	kJ/mol	NIST
PAff	805.00 ± 6.70	kJ/mol	NIST
BasG	[775.60; 776.30]	kJ/mol
BasG	775.60	kJ/mol	NIST
BasG	776.30 ± 2.70	kJ/mol	NIST
BasG	776.30 ± 2.70	kJ/mol	NIST
ΔcH°gas	[-2722.00; -2699.50]	kJ/mol
ΔcH°gas	-2699.50 ± 1.00	kJ/mol	NIST
ΔcH°gas	-2722.00	kJ/mol	NIST
ΔfG°	62.09	kJ/mol	Joback Calculated Property
ΔfH°gas	-17.90 ± 1.10	kJ/mol	NIST
ΔfusH°	3.53	kJ/mol	Joback Calculated Property
ΔvapH°	20.60	kJ/mol	NIST
IE	[9.17; 9.45]	eV
IE	9.22 ± 0.02	eV	NIST
IE	9.19	eV	NIST
IE	9.24 ± 0.05	eV	NIST
IE	9.24 ± 0.02	eV	NIST
IE	9.24 ± 0.00	eV	NIST
IE	9.19	eV	NIST
IE	9.21	eV	NIST
IE	9.17	eV	NIST
IE	9.23 ± 0.02	eV	NIST
IE	9.23	eV	NIST
IE	9.41	eV	NIST
IE	9.39	eV	NIST
IE	Outlier 9.45	eV	NIST
log10WS	[-2.33; -2.33]
log10WS	-2.33		Aq. Solubility Prediction
log10WS	-2.33		Estimated Solubility
logPoct/wat	1.582		Crippen Calculated Property
McVol	62.920	ml/mol	McGowan Calculated Property
Pc	[4000.00; 4009.80]	kPa
Pc	4009.80	kPa	Thermodynamic properties of the butenes Part I. Experimental densities, vapor pressures, and critical points
Pc	4000.00 ± 10.00	kPa	NIST
Pc	4000.31 ± 10.13	kPa	NIST
ρc	[233.96; 235.09]	kg/m3
ρc	235.09 ± 0.56	kg/m3	NIST
ρc	233.96 ± 2.81	kg/m3	NIST
Inp	[370.00; 400.00]
Inp	394.00		NIST
Inp	391.00		NIST
Inp	389.00		NIST
Inp	390.00		NIST
Inp	390.00		NIST
Inp	390.00		NIST
Inp	380.00		NIST
Inp	383.00		NIST
Inp	383.00		NIST
Inp	383.00		NIST
Inp	384.00		NIST
Inp	390.00		NIST
Inp	382.00		NIST
Inp	392.00		NIST
Inp	391.00		NIST
Inp	384.00		NIST
Inp	383.00		NIST
Inp	Outlier 400.00		NIST
Inp	385.00		NIST
Inp	Outlier 370.00		NIST
Inp	388.00		NIST
Inp	386.00		NIST
Inp	384.00		NIST
Inp	390.00		NIST
Inp	383.00		NIST
Inp	387.00		NIST
Inp	388.00		NIST
Inp	390.00		NIST
Inp	390.00		NIST
Inp	383.00		NIST
I	[427.00; 438.00]
I	438.00		NIST
I	427.00		NIST
S°gas	293.59	J/mol×K	NIST
S°liquid	194.00	J/mol×K	NIST
Tboil	[266.20; 269.15]	K
Tboil	266.26	K	NIST
Tboil	266.30	K	NIST
Tboil	268.15 ± 1.50	K	NIST
Tboil	267.15 ± 1.50	K	NIST
Tboil	Outlier 268.65 ± 1.50	K	NIST
Tboil	266.40 ± 0.50	K	NIST
Tboil	267.15 ± 1.00	K	NIST
Tboil	267.15 ± 1.00	K	NIST
Tboil	266.55 ± 0.70	K	NIST
Tboil	266.35 ± 0.50	K	NIST
Tboil	266.65 ± 2.00	K	NIST
Tboil	266.26 ± 0.55	K	NIST
Tboil	266.55 ± 0.30	K	NIST
Tboil	266.22 ± 0.20	K	NIST
Tboil	267.15 ± 2.00	K	NIST
Tboil	267.15 ± 2.00	K	NIST
Tboil	266.55 ± 1.00	K	NIST
Tboil	266.45 ± 0.50	K	NIST
Tboil	267.15 ± 2.00	K	NIST
Tboil	266.85 ± 1.00	K	NIST
Tboil	266.20 ± 0.50	K	NIST
Tboil	267.15 ± 1.50	K	NIST
Tboil	266.35 ± 0.20	K	NIST
Tboil	266.55 ± 0.50	K	NIST
Tboil	266.55 ± 2.00	K	NIST
Tboil	267.15 ± 2.00	K	NIST
Tboil	Outlier 269.15 ± 2.00	K	NIST
Tboil	267.15 ± 2.00	K	NIST
Tc	[417.88; 420.15]	K
Tc	417.90 ± 0.10	K	NIST
Tc	417.88 ± 0.10	K	NIST
Tc	420.15 ± 2.00	K	NIST
Tfus	[125.40; 132.95]	K
Tfus	132.95	K	Aq. Solubility Prediction
Tfus	132.38	K	NIST
Tfus	132.45 ± 0.30	K	NIST
Tfus	125.40 ± 0.50	K	NIST
Ttriple	[132.40; 132.40]	K
Ttriple	132.40 ± 0.20	K	NIST
Ttriple	132.40 ± 0.20	K	NIST
Vc	0.239	m3/kmol	NIST

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[75.86; 100.25]	J/mol×K	[239.15; 353.15]
Cp,gas	75.86 ± 0.38	J/mol×K	239.15	NIST
Cp,gas	82.89 ± 0.41	J/mol×K	272.15	NIST
Cp,gas	91.67 ± 0.46	J/mol×K	312.15	NIST
Cp,gas	100.25 ± 0.50	J/mol×K	353.15	NIST
Cp,liquid	[106.80; 121.42]	J/mol×K	[140.00; 266.26]
Cp,liquid	106.80	J/mol×K	140.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	107.30	J/mol×K	150.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	108.00	J/mol×K	160.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	108.90	J/mol×K	170.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	109.90	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	111.10	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	112.40	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	113.90	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	115.50	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	117.20	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	118.90	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	120.80	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	121.42	J/mol×K	253.10	NIST
Cp,liquid	121.30	J/mol×K	266.26	NIST
ΔfusH	[5.92; 5.92]	kJ/mol	[132.40; 132.40]
ΔfusH	5.92	kJ/mol	132.40	NIST
ΔfusH	5.92	kJ/mol	132.40	NIST
ΔfusH	5.92	kJ/mol	132.40	NIST
ΔfusH	5.92	kJ/mol	132.40	NIST
ΔvapH	[22.20; 23.10]	kJ/mol	[244.50; 394.50]
ΔvapH	22.80	kJ/mol	244.50	NIST
ΔvapH	23.10	kJ/mol	245.50	NIST
ΔvapH	22.70	kJ/mol	289.50	NIST
ΔvapH	22.20	kJ/mol	343.00	NIST
ΔvapH	22.20	kJ/mol	350.50	NIST
ΔvapH	22.30	kJ/mol	394.50	NIST
Pvap	[133.00; 1546.60]	kPa	[273.15; 364.52]
Pvap	133.00	kPa	273.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	133.00	kPa	273.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	224.00	kPa	288.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	223.00	kPa	288.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	224.00	kPa	288.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	352.00	kPa	303.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	353.00	kPa	303.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	353.00	kPa	303.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	413.70	kPa	308.13	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	467.10	kPa	312.59	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	466.10	kPa	312.59	Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
Pvap	465.30	kPa	312.60	Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
Pvap	538.00	kPa	318.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	536.00	kPa	318.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	538.00	kPa	318.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	542.10	kPa	318.35	Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	538.15	kPa	318.40	Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
Pvap	605.14	kPa	322.79	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	607.94	kPa	323.07	Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
Pvap	608.94	kPa	323.11	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	609.14	kPa	323.14	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	608.84	kPa	323.14	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	611.04	kPa	323.15	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap	787.00	kPa	333.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	785.00	kPa	333.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	787.00	kPa	333.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	855.50	kPa	336.84	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	1054.90	kPa	346.14	Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	1110.00	kPa	348.15	(Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
Pvap	1107.00	kPa	348.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	1110.00	kPa	348.15	Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
Pvap	1154.30	kPa	350.43	Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
Pvap	1515.00	kPa	363.15	Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
Pvap	1546.00	kPa	364.49	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
Pvap	1546.50	kPa	364.51	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
Pvap	1546.60	kPa	364.51	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
Pvap	1546.20	kPa	364.51	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	1546.30	kPa	364.52	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
ΔfusS	[44.71; 44.71]	J/mol×K	[132.40; 132.40]
ΔfusS	44.71	J/mol×K	132.40	NIST
ΔfusS	44.71	J/mol×K	132.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[191.15; 285.02]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.40957e+01
Coefficient B			-2.26626e+03
Coefficient C			-2.70260e+01
Temperature range, min.			191.15
Temperature range, max.			285.02
Pvap	1.33	kPa	191.15	Calculated Property
Pvap	3.04	kPa	201.58	Calculated Property
Pvap	6.33	kPa	212.01	Calculated Property
Pvap	12.16	kPa	222.44	Calculated Property
Pvap	21.89	kPa	232.87	Calculated Property
Pvap	37.23	kPa	243.30	Calculated Property
Pvap	60.29	kPa	253.73	Calculated Property
Pvap	93.58	kPa	264.16	Calculated Property
Pvap	139.97	kPa	274.59	Calculated Property
Pvap	202.66	kPa	285.02	Calculated Property
Pvap	[6.66e-04; 4013.56]	kPa	[132.81; 417.90]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.75294e+01
Coefficient B			-4.53316e+03
Coefficient C			-8.37142e+00
Coefficient D			1.22482e-05
Temperature range, min.			132.81
Temperature range, max.			417.90
Pvap	6.66e-04	kPa	132.81	Calculated Property
Pvap	0.09	kPa	164.49	Calculated Property
Pvap	2.01	kPa	196.16	Calculated Property
Pvap	16.84	kPa	227.84	Calculated Property
Pvap	77.59	kPa	259.52	Calculated Property
Pvap	244.97	kPa	291.19	Calculated Property
Pvap	603.20	kPa	322.87	Calculated Property
Pvap	1256.40	kPa	354.55	Calculated Property
Pvap	2334.76	kPa	386.22	Calculated Property
Pvap	4013.56	kPa	417.90	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propene, 2-methyl-.

Mixtures

• 1-Propene, 2-methyl- + Propanenitrile
• 1-Propene, 2-methyl- + Ethyl Acetate
• Dimethyl sulfide + 1-Propene, 2-methyl-
• Ethane, 1,1,1-trifluoro- + 1-Propene, 2-methyl-
• 1-Propene, 2-methyl- + 1-Pentanol
• 1-Propene, 2-methyl- + 2-Pentanol
• 1-Propene, 2-methyl- + 3-Pentanol
• 1-Propanol + 1-Propene, 2-methyl-
• 1-Propene, 2-methyl- + Diethyl sulfide
• 1-Propene, 2-methyl- + Ethane, 1,1-difluoro-
• 1-Propene, 2-methyl- + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + 1-Propene, 2-methyl-
• 1-Propene, 2-methyl- + Methyl Alcohol
• 1-Propene, 2-methyl- + Tetrahydropyran
• 1-Propene, 2-methyl- + 2-Methyl-1-butanol
• 1-Propene, 2-methyl- + 1-Butanol, 3-methyl-
• 1-Propene, 2-methyl- + Amylene hydrate
• Allyl alcohol + 1-Propene, 2-methyl-
• 1-Propene, 2-methyl- + Acetone
• 2-Propanol + 1-Propene, 2-methyl-

Find more mixtures with 1-Propene, 2-methyl-.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Thermodynamic properties of the butenes Part I. Experimental densities, vapor pressures, and critical points
• Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
• Henry s law constants of 1-butene, 2-methylpropene, trans-2-butene, and 1,3-butadiene in methanol at 374 490K
• Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
• Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system
• Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
• Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• (Vapour + liquid) equilibria of the {1,1,1-trifluoroethane (HFC-143a) + isobutene} system
• Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
• Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
• Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
• Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
• Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
• Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
• Vapor-Liquid Equilibria of the 1,1,1,2,3,3,3-Heptafluoropropane + Isobutene System
• Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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